Catalyst system and process for the production of polyethylenes

1. A catalyst system for the production of polyethylene comprising:

I) the reaction product obtained by reacting

a) a hydrocarbon solution comprising:

i. a magnesium-containing compound selected from an organic oxygen-containing magnesium compound and/or a halogen-containing magnesium compound; and

ii. an organic oxygen-containing titanium compound

wherein the molar ratio of magnesium:titanium is lower than 3:1;

and

b) an organo aluminium halide having the formula AlR n X 3-n in which R is a hydrocarbon moiety containing 1-10 carbon atoms, X is a halogen and 0<n<3;

II) an aluminium compound having the formula AlR′ 3 , in which R′ is a hydrocarbon moiety containing 1-10 carbon atoms; and

III) an electron donor selected from the group of 1,2-dialkoxy hydrocarbon compounds

wherein

the molar ratio of supplied organo aluminium halide I)b) to supplied titanium in I)a) in the preparation of I) is between 5.0 and 7.0; and

the molar ratio of the one or more of an electron donor III) to the titanium present in the reaction product I) is between 0.05 and 0.40.

2. The catalyst system according to claim 1 wherein the electron donor III) comprises an external electron donor.

3. The catalyst system according to claim 1 , for the production of polyethylene wherein the production of polyethylene is performed in a slurry polymerisation process.

4. The catalyst system according to claim 1 , wherein the electron donor is selected from the group of 1,2-dialkoxy hydrocarbon compounds represented by the formula (I):

wherein C 1 -C 2 is a connecting group consisting of 2 carbon atoms which are in the sp 3 and/or sp 2 hybridisation form and wherein the substituents R and R′ are hydrocarbon groups with 1-10 carbon atoms and may be the same or different and may optionally be substituted with other heteroatom-containing groups.

5. The catalyst according to claim 1 , wherein the electron donor is selected from the group of 1,2-dialkoxy hydrocarbon compounds of formula (II) or (III):

wherein the substituents R″ are selected from hydrocarbon groups with 1-10 carbon atoms or hydrogen and may be the same or different and may optionally be substituted with other heteroatom-containing groups, and may join with one or more of other substituents R″ to form cyclic groups.

6. The catalyst system according to claim 1 , wherein the electron donor is selected from 1,2-dimethoxybenzene, 1,2,4-trimethoxybenzene, 1,2-diethoxybenzene, 2,3-dimethoxytoluene, 1-allyl-3,4-dimethoxybenzene, 1,2-dimethoxyethane, 1,2-dimethoxy cyclohexane, 1,2-dimethoxypropane, 1,2-dimethoxybutane, or 2,3-dimethoxybutane.

7. A process for the production of a polyethylene, the process comprising polymerizing ethylene in the presence of the catalyst system according to claim 1 to produce a polyethylene, wherein the polyethylene has a density of ≥935 kg/m 3 and ≤975 kg/m 3 as measured in accordance with ISO 1183-1 (2012), method A.

8. The process according to claim 7 wherein the polyethylene is a multimodal polyethylene.

9. The process for the production of polyethylene according to claim 7 , wherein the process is a multi-stage slurry polymerisation process comprising at least two stages.

10. The process according to claim 9 wherein ingredient I) and II) of the catalyst system are introduced in the first stage of said multi-stage polymerisation process, and wherein ingredient III) is introduced in any of the stages of said multi-stage slurry polymerisation process.

11. The process according to claim 7 , wherein the polyethylene has a melt flow rate of greater than or equal to 60.0 g/10 min, as determined in accordance with ISO 1133-1 (2011), at a temperature of 190° C. and a load of 21.6 kg.

12. The process according to claim 7 , wherein the polyethylene has a hexane-extractable content of less than 2.00 wt %.

13. The process according to claim 12 , wherein the hexane-extractable content is less than 1.50 wt %.

14. The process according to claim 7 , wherein a fraction of ethane formed during polymerization is lower than 0.25 volume percent.

15. The process according to claim 7 ,

wherein a fraction of ethane formed during polymerization is lower than 0.30 volume percent;

wherein the polyethylene has a hexane-extractable content is less than 2.00 wt %; and

wherein the polyethylene has a melt flow rate of greater than or equal to 60.0 g/10 min, as determined in accordance with ISO 1133-1 (2011), at a temperature of 190° C. and a load of 21.6 kg.

16. The process according to claim 15 , wherein the hexane-extractable content is less than 1.50 wt %.

17. The process according to claim 15 , wherein a fraction of ethane formed during polymerization is lower than 0.25 volume percent.

18. The catalyst system according to claim 1 , wherein:

the magnesium-containing compound is magnesium ethoxide;

the organic oxygen-containing titanium compound is Ti(OC 4 H 9 ) 4 , the molar ratio of magnesium:titanium is equal to or greater than 1.5:1 and lower than 3:1;

the organo aluminium halide having the formula AlR n X 3-n is ethyl aluminium dichloride;

the aluminium compound having the formula AlR′ 3 is trietyl aluminium or triisobutyl aluminium; and

the electron donor is selected from the group consisting of 1,2-dimethoxybenzene and 1-allyl-3,4-dimethoxybenzene.